J. L. T. Azevedo

ORCID: 0000-0002-8415-2786
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About
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Research Areas
  • Thermochemical Biomass Conversion Processes
  • Combustion and flame dynamics
  • Radiative Heat Transfer Studies
  • Coal Properties and Utilization
  • Iron and Steelmaking Processes
  • Granular flow and fluidized beds
  • Catalysts for Methane Reforming
  • Catalytic Processes in Materials Science
  • Fire dynamics and safety research
  • Forest Biomass Utilization and Management
  • Heat transfer and supercritical fluids
  • Process Optimization and Integration
  • Metallurgical Processes and Thermodynamics
  • Hydrogen Storage and Materials
  • Coal Combustion and Slurry Processing
  • Particle Dynamics in Fluid Flows
  • Cyclone Separators and Fluid Dynamics
  • Combustion and Detonation Processes
  • Spacecraft and Cryogenic Technologies
  • Coal and Coke Industries Research
  • Advancements in Solid Oxide Fuel Cells
  • Flame retardant materials and properties
  • Materials Engineering and Processing
  • Lignin and Wood Chemistry
  • Energy and Environment Impacts

Instituto Superior Técnico
1993-2016

Instituto Politécnico de Lisboa
1997-2015

University of Lisbon
2000-2014

Friedrich-Alexander-Universität Erlangen-Nürnberg
1988

Abstract Measurements have been performed in a 300 MWe, front-wall-fired, pulverized-coal, utility boiler. This boiler was retrofitted with boosted over fire air injectors that allowed the operation of furnace under deeper staging conditions. New data are reported for local mean gas species concentration O2, CO, CO2, NOx, temperatures and char burnout measured at several ports including those main combustion staged regions. Comparisons present our previous measurements this boiler, prior to...

10.1080/00102200701385042 article EN Combustion Science and Technology 2007-07-30

Measurements have been performed in a 300-MW e , front-wall-fired, pulverized-coal utility boiler. New data are reported for local mean gas species concentrations of O 2 CO, CO and NO x temperatures, charburnout measured at several ports the boiler including those burner region. They complement previously obtained same before being retrofitted with low-NO burners over-fire air ports. During current experimental work, considerable effort was made to assure minimum variations on operating...

10.1080/00102200302404 article EN Combustion Science and Technology 2003-02-01

10.1016/s0045-7825(00)00287-5 article EN Computer Methods in Applied Mechanics and Engineering 2001-03-01

Abstract This paper describes the results of an experimental study undertaken in 300 M We front-wall-fired, pulverized-coal, utility boiler. The data reported include local mean gas species concentrations O2, CO, CO2, NOx,, and temperatures measured at several ports boiler including those burner region, incident wall heat fluxes taken around periphery 39 ports. duxes are for two operating conditions. During work here, a considerable effort was made to assure minimum variations on conditions...

10.1080/00102209708935729 article EN Combustion Science and Technology 1997-11-01

10.1016/s0082-0784(00)80632-3 article EN Proceedings of the Combustion Institute 2000-01-01

This paper describes an experimental and numerical investigation on the co-combustion of propane with pulverized coal, pine shells, textile wastes. Measurements have been performed in a large-scale laboratory furnace fired by industrial-type swirl burner. Data are reported for in-flame major gas-phase species concentration, including NOx, gas temperature, overall char burnout three flames: propane/coal flame, propane/pine shells propane/textile wastes flame. For comparison purposes, data...

10.1080/00102200490514886 article EN Combustion Science and Technology 2004-12-01

ABSTRACT In this paper a mathematical model to describe Circulating Atmospheric Fluidised Bed Combustor (CAFBC) is presented. For the fast section of bed, momentum and energy balance equations are used predict temperature velocity profiles for gas particles. The performs mass balances chemical species (O2, H2O, CO2, CO SO2) with consideration on last being given retention by limestone A bubbling bed considered simulate bottom CAFBC. applied typical conditions boiler results show expected trends

10.1080/00102209308935291 article EN Combustion Science and Technology 1993-09-01

Abstract Numerical predictions of two‐phase turbulent gas‐particle flows are reported for two test cases: a plane jet and an axisymmetric free jet. The numerical algorithm uses Eulerian approach the fluid phase particulate is described by using Lagrangian stochastic model. k ‐ε turbulence model was used to characterize length time scales fluid. In confined influence restitution coefficient on statistical distribution velocities analysed. Particular attention dedicated ε equation corrections...

10.1002/ppsc.19900070131 article EN Particle & Particle Systems Characterization 1990-01-01
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